EP0266808B1 - Process for delaying and controlling the formation of gels or precipitates derived from aluminum and corresponding compositions together with its applications particularly those concerning the operation of oil wells - Google Patents
Process for delaying and controlling the formation of gels or precipitates derived from aluminum and corresponding compositions together with its applications particularly those concerning the operation of oil wells Download PDFInfo
- Publication number
- EP0266808B1 EP0266808B1 EP19870201737 EP87201737A EP0266808B1 EP 0266808 B1 EP0266808 B1 EP 0266808B1 EP 19870201737 EP19870201737 EP 19870201737 EP 87201737 A EP87201737 A EP 87201737A EP 0266808 B1 EP0266808 B1 EP 0266808B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- aluminum
- per
- activator
- formation
- gels
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/50—Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
- C09K8/504—Compositions based on water or polar solvents
- C09K8/5045—Compositions based on water or polar solvents containing inorganic compounds
Definitions
- This invention covers compositions which make it possible to retard and control the formation of gels or precipitates derived from aluminum, and has applications for the operation of oil wells.
- a second possibility lies in the introduction of a fluid designed to react with a particular component of the reservoir, such as inherent water in the latter, to form an insoluble precipitate.
- the specialist is referred to US Patent No. 3,837,400.
- the time required for the formation of the gel or precipitate determines the possible degree of penetration into the formation, while the morphology of the solid phase defines the degree by which the permeability of the formation is reduced.
- US Patent No. 3,614,985 describes the precipitation of metal hydroxides such as chromium hydroxide or aluminum hydroxide in a homogeneous solution.
- the previously cited patent describes the delayed formation of aluminum hydroxide-type compounds by employing a solution consisting of a suitable aluminum salt, and an activator.
- the activator is used to slowly increase the pH level within the temperature ranges normally found at the well bottom. This in turn leads to the slow formation of an insoluble hydroxide phase.
- a suitable activator is urea, which undergoes hydrolosis at high temperatures to form ammonia which consequently raises the pH of the solution.
- the solid aluminum hydroxide precipitate phase has a tendency to remain amorphous, with the consistency of a gel.
- Typical treatment solutions (approximately 0.05 to 0.15 M A1 3+) have a pH of about 3 and, as recommended in the above patent, it is preferable to adjust the pH to about 4.
- a pH of 3 fluid interaction with the carbonate present in the porous medium is very rapid and limits peneration of the fluid into the matrix.
- a pH of 3 requires a strong concentration of urea to start the precipitation reaction and thus a pH of 4 is preferable.
- LOCRON is an aluminum hydroxychloride corresponding to the above-mentioned formula, which is marketed by the firm of HOECHST AG, Frankfurt, West Germany.
- the concentration of urea and sodium cyanate varies in the manner shown on the attached figure, which gived the gelling time variation according to the cyanate concentration for urea concentrations of between 9 and 3% by weight.
- the brine is typical of those found in the field.
- the gelling time is measured at a temperature of 50.C (122.F). Examination of the curved obtained shows that the gelling time can easily be controlled from about 1 to 2 hours to more than 80 hours.
- the aluminum hydroxychloride content must be at least 2% by weight.
- the effective concentration of cyanate is about 500 to 1500 ppm.
- Example A The operations are the same as for Example A, with the urea being replaced by hexamethylenetetramine.
- the results are given in the table below and show that hexamethylenetetramine can largely be used in the same way as urea.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
Description
- This invention covers compositions which make it possible to retard and control the formation of gels or precipitates derived from aluminum, and has applications for the operation of oil wells.
- During the production of hydrocarbons from underground formations, it is often desirable to reduce the permeability of certain zones in the formation. This is the case, for example, when a formation neighboring on the production well is likely todirect water into the well. Another example is where zones of high permeability are neighboring on the injection wells.
- One method of reducing the permeability of certain undergound zones consists in precipitating a product in-situ. This technique is well understood and is usually employed by the placing of two incompatible fluids inside the reservoir. This leads to the formation of a precipitate, giving reduced permeability wherever the two fluids come into contact and mix inside the reservoir. The specialist is referred to US Patents, Nos. 3,837,400 -4,031,958 and 4,304,301.
- A second possibility lies in the introduction of a fluid designed to react with a particular component of the reservoir, such as inherent water in the latter, to form an insoluble precipitate. The specialist is referred to US Patent No. 3,837,400.
- Another technique consists yet again in introducing a fluid with the intrinsic potential of creating a precipitate or gel, such formation however requiring retardment by some means. The specialist is referred to US Patents, Nos 4,413,680 and 3,614,985.
- In order to master the operation, it is essential that two parameters are controlled: the time required for the formation of the gel or precipitate and the morphology of the solid phase subsequently produced. This is because the time taken for the reaction determines the possible degree of penetration into the formation, while the morphology of the solid phase defines the degree by which the permeability of the formation is reduced.
- US Patent No. 3,614,985 describes the precipitation of metal hydroxides such as chromium hydroxide or aluminum hydroxide in a homogeneous solution.
- Numerous simple salts of aluminum III (such as aluminum chloride or aluminum nitrate) are soluble in slightly acid mediums, but form insoluble aluminum hydroxides when the pH level goes beyond about 5.
- The previously cited patent describes the delayed formation of aluminum hydroxide-type compounds by employing a solution consisting of a suitable aluminum salt, and an activator. The activator is used to slowly increase the pH level within the temperature ranges normally found at the well bottom. This in turn leads to the slow formation of an insoluble hydroxide phase. As stated in this document, a suitable activator is urea, which undergoes hydrolosis at high temperatures to form ammonia which consequently raises the pH of the solution. The solid aluminum hydroxide precipitate phase has a tendency to remain amorphous, with the consistency of a gel.
- The only example of a practical system described in the above mentioned patent concerns the precipitation of aluminum hydroxide from aluminum chloride. However, the way it is described, this solution does not have a practical application in oilfield operations because of both safety and technical constraints. In fact, aluminum chloride in solid form reacts violently with water, giving off heat and hydrochloric acid vapors.
- Such a system would therefore be extremely dangerous to handle in the field. In addition, the use of concentrated solutions of aluminum chloride is not desirable on account of the volume of fluid required and the need to employ a corrosion inhibitor to protect the fluid-metering pumps. It is an established fact that corrosion inhibitors often affect well treatment.
- Typical treatment solutions (approximately 0.05 to 0.15 M A1 3+) have a pH of about 3 and, as recommended in the above patent, it is preferable to adjust the pH to about 4. In fact, with a pH of 3, fluid interaction with the carbonate present in the porous medium is very rapid and limits peneration of the fluid into the matrix. Even in the case of a very pure sandstone, where reaction with carbonates is not a problem, a pH of 3 requires a strong concentration of urea to start the precipitation reaction and thus a pH of 4 is preferable.
- Unfortunately this pH adjustment is impossible, or at best impractical, with the system described in the above patent. The addition of an alkaline agent to a typical aluminum chloride solution in fact produces immediate and inevitable precipitation, and while this precipitation does dissolve slowly over a period of time and lead to a higher pH, its presence requires the use of intermittent mixing techniques. These can only be applied to large volumes of fluid, with operations lasting several days or weeks, particularly as the operations are performed in very restricted areas. The preceding process is valid when fresh water is available. Where the mix water employed is not pure, but rather the classic brine solution found on oilfields, whether brine proper or sea water etc., the initial precipitate formed by the addition of the alkaline agent does not dissolve, even when energetically mixed at high temperatures over a long period. In such cases, which are all too frequent, there is no solution to the problem.
- An important step was taken with Main Application FR-A-85.10272, lodged 2 July 1985, which describes the use of an aluminum hydroxychloride. This polymer salt is produced commercially by the electrolysis of aluminum chloride solutions. Its formula in the crystalline form is :
[Al₂(OH)₅Cl, 2.5H₂O]n
More usually it has the form of a partially neutralized acid aluminum salt, with the general formula :
Aln(OH)mXp
in which X in a mineral or organic anion, or a mixture of mineral and organic anions, with (pxq) + m = 3n, q begin the valency of the anion, the ratio (m/3n) x 100 defining the basicity of the said salt and situated between 30 and 80 %. - Use of an aluminum hydroxychloride as a plugging agent makes it possible to solve the problems encountered with previous techniques and also offers the specialist new possiblities, especially in connection with the effective control of the gelling or precipitation time and monitoring the morphology of the precipitate.
- The specialist can refer to the application for above-mentioned French Patent No. 85-10272, the details of which are included here as a reference.
- According to this application, it is shown that weak cases other than urea can be used as "acitvators", especially hexametheylenetetramine (activator) in combination with an aluminum hydroxychloride used as a plugging agent.
- This invention has now shown that the reaction of the activator is markedly improved by the simultaneous use of sodium cyanate as an activator aid. The two main advantages given by the addition of sodium cycanate are :
- 1. Better performance of the system at low temperature (< 50.C or < 122. F) and,
- 2. Greater flexibility in the control of the gelling time.
- The specialist will appreciate these two advantages in taking the following two non-limiting examples.
- Note: "LOCRON" is an aluminum hydroxychloride corresponding to the above-mentioned formula, which is marketed by the firm of HOECHST AG, Frankfurt, West Germany.
- Different solutions are prepared in a brine containing the "LOCRON"® aluminum hydroxychloride as plugging agent, with the activator being urea in combination with sodium cyanate. the concentration of aluminum hydroxide is 3% by weight.
- The concentration of urea and sodium cyanate varies in the manner shown on the attached figure, which gived the gelling time variation according to the cyanate concentration for urea concentrations of between 9 and 3% by weight. The brine is typical of those found in the field.
- The gelling time is measured at a temperature of 50.C (122.F). Examination of the curved obtained shows that the gelling time can easily be controlled from about 1 to 2 hours to more than 80 hours. The aluminum hydroxychloride content must be at least 2% by weight. The effective concentration of cyanate is about 500 to 1500 ppm.
- The fact of having used a brine with 3% NaCl for the tests, confirms the compatibility of the system with saline mediums which is also an important advantage. In fact the system will operate up to at least 10% NaCl. Beyond this the gel is likely to be less strong.
- The operations are the same as for Example A, with the urea being replaced by hexamethylenetetramine. The results are given in the table below and show that hexamethylenetetramine can largely be used in the same way as urea.
- The following formuala is used, prepared according to the invention :
approx. 3% by weight of aluminum hydroxychloride
approx. 3 - 9% by weight of urea
approx. 1000 ppm of sodium cyanate.TABLE Test temperature : 50.C (122.F)
Brine at 1% NaClSodium Cyanate (ppm) Hexamethylenetetramine (ppm) Gel time 1000 5000 20 H 1000 4000 40 H 1000 3000 90 H 1100 4000 30 H 1100 3000 60 H 1100 2000 110 H 1200 3500 40 H 1200 3000 60 H 1500 2500 60 H
Claims (9)
- Process for delaying and controlling the formation of gels and precipitates derived from aluminum, in which a starting product consisting of a partially neutralized acid salt of aluminum, with the general formula:
Aln(OH)m.Xp
(in which X is a mineral or oragnic anion, or a mixture of mineral or organic anions, with (p x q) + m = 3n, q being the valency of the anion, the ratio (m/3n) x 100 defining the basicity of the said salt and situated between 30 and 80%), is submitted to the reaction of a weak-base activator, and characterized by employment in the activator, of sodium cyanate acting as an activator aid. - Process as per Claim 1, characterized by the fact that the said starting product is an aluminum hydroxychloride with the formula 1
Al₂(OH)₅ Cl, 2,5 H₂O
- Process as per Claims 1 or 2, characterized by the use of hexamethylenetetramine as activator.
- Process as per Claims 1 or 2, characterized by the use of urea as activator.
- Process as per any of Claims 1 to 4, characterized by a cyanate concentration of between 500 and 1500 ppm.
- Process as per Claims 5, characterized by a urea concentration of 3 to 9%.
- Process as per Claim 5 or 6, characterized by an aluminum hydroxychloride concentration in the order of 3%.
- Gelling or precipitation retarding compositions obtained by the process of any of Claims 1 to 7.
- Applications of the compositions according to claim 8 for the plugging of underground formations, particularly as regards the boring of oil wells or similar.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8614089 | 1986-10-08 | ||
FR8614089A FR2604989B1 (en) | 1986-10-08 | 1986-10-08 | PROCESS FOR DELAYING AND CONTROLLING THE FORMATION OF GELS OR PRECIPITES OF ALUMINUM DERIVATIVES, COMPOSITIONS THEREOF AND APPLICATIONS IN PARTICULAR FOR THE EXPLOITATION OF OIL WELLS |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0266808A1 EP0266808A1 (en) | 1988-05-11 |
EP0266808B1 true EP0266808B1 (en) | 1992-03-18 |
Family
ID=9339729
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19870201737 Expired - Lifetime EP0266808B1 (en) | 1986-10-08 | 1987-09-11 | Process for delaying and controlling the formation of gels or precipitates derived from aluminum and corresponding compositions together with its applications particularly those concerning the operation of oil wells |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0266808B1 (en) |
DE (1) | DE3777534D1 (en) |
FR (1) | FR2604989B1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2642467B1 (en) * | 1989-01-27 | 1991-04-26 | Schlumberger Cie Dowell | DELAYED RIGID FOAM SYSTEMS AND APPLICATIONS IN PARTICULAR TO SELECTIVE CLOGGING TREATMENTS IN THE OIL INDUSTRY |
FR2642468B1 (en) * | 1989-01-27 | 1991-04-26 | Schlumberger Cie Dowell | FOAM SYSTEMS FOR SELECTIVE SEALING OF SUBTERRANEAN FORMATIONS, ESPECIALLY AROUND OIL WELLS |
US7501385B2 (en) | 2004-06-15 | 2009-03-10 | Halliburton Energy Services, Inc. | Compositions and methods for water control and strengthening unconsolidated formations |
EP2436748B1 (en) * | 2010-10-04 | 2013-06-05 | Wintershall Holding GmbH | Method for producing crude oil from subterranean crude oil storage areas |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3614985A (en) * | 1970-03-30 | 1971-10-26 | Shell Oil Co | Plugging a subterranean formation by homogeneous solution precipitation |
FR2150637A1 (en) * | 1971-09-03 | 1973-04-13 | Chevron Res | Maintaining formation permeability withhydro |
FR2584387B1 (en) * | 1985-07-02 | 1987-10-23 | Schlumberger Cie Dowell | PROCESS FOR DELAYING AND CONTROLLING THE FORMATION OF GELS OR PRECIPITES OF ALUMINUM DERIVATIVES, COMPOSITIONS THEREOF AND APPLICATIONS IN PARTICULAR FOR THE EXPLOITATION OF OIL WELLS |
-
1986
- 1986-10-08 FR FR8614089A patent/FR2604989B1/en not_active Expired
-
1987
- 1987-09-11 EP EP19870201737 patent/EP0266808B1/en not_active Expired - Lifetime
- 1987-09-11 DE DE8787201737T patent/DE3777534D1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0266808A1 (en) | 1988-05-11 |
FR2604989B1 (en) | 1988-12-09 |
DE3777534D1 (en) | 1992-04-23 |
FR2604989A1 (en) | 1988-04-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4779680A (en) | Hydraulic fracturing process using a polymer gel | |
US4343363A (en) | Process for cleaning a subterranean injection surface and for selectively reducing the permeability of a subterranean formation | |
US4989673A (en) | Lost circulation fluid for oil field drilling operations | |
US4498539A (en) | Selective plugging of highly permeable subterranean strata by in situ _gelation of polymer solutions | |
US4552217A (en) | Microbiocidal anionic sequesterants with polyvalent metal cations for permeability correction process | |
US4304677A (en) | Method of servicing wellbores | |
CA1282582C (en) | Rate-controlled polymer gelation process for oil recovery applications | |
CA1282685C (en) | Preventing plugging by insoluble salts in a hydrocarbon-bearingformation and associated production wells | |
US7104327B2 (en) | Methods of fracturing high temperature subterranean zones and foamed fracturing fluids therefor | |
WO2001000746A1 (en) | Compositions and processes for oil field applications | |
EP0599474B1 (en) | Controlling iron in aqueous well fracturing fluids | |
US4889563A (en) | Process for retarding and controlling the formation of gels or precipitates derived from aluminium and corresponding compositions, plus the corresponding applications-in particular regarding oil wells | |
WO1995018909A1 (en) | Hydrocarbon recovery process utilizing a gel prepared from a polymer and a preformed crosslinking agent | |
US4762178A (en) | Oil recovery with water containing carbonate salt and CO2 | |
CA1282581C (en) | Polymer gelation process for oil recovery applications | |
EP0266808B1 (en) | Process for delaying and controlling the formation of gels or precipitates derived from aluminum and corresponding compositions together with its applications particularly those concerning the operation of oil wells | |
US6123869A (en) | Precipitation of scale inhibitors | |
US4693310A (en) | Conformance correction to improve hydrocarbon recovery from a subterranean formation | |
CA2193038C (en) | A process for the controlled fixing of scale inhibitor in a subterranean formation | |
US4287951A (en) | Process for improving conformance and flow profiles in a subterranean sandstone formation | |
US4503912A (en) | Process for conformance control using a polymer flocculate | |
US4301867A (en) | Process for selectively reducing the permeability of a subterranean sandstone formation | |
US4629747A (en) | Microbiocidal anionic sequesterants with polyvalent metal cations for permeability correction process | |
US3902556A (en) | Secondary oil recovery method | |
US5816323A (en) | Permeability reduction in a hydrocarbon-bearing formation using a stabilized polymer gel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE GB IT NL |
|
17P | Request for examination filed |
Effective date: 19880912 |
|
17Q | First examination report despatched |
Effective date: 19900913 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE GB IT NL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRE;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.SCRIBED TIME-LIMIT Effective date: 19920318 Ref country code: NL Effective date: 19920318 |
|
REF | Corresponds to: |
Ref document number: 3777534 Country of ref document: DE Date of ref document: 19920423 |
|
NLV1 | Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19930602 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20010912 Year of fee payment: 15 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20020911 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20020911 |